System for recirculating the exhaust of a turbomachine

ABSTRACT

A portion of the exhaust generated by a turbomachine is recirculated through an inlet portion by an exhaust gas recirculation system. The system reduces the level of harmful constituents within the exhaust before the exhaust is recirculated.

BACKGROUND OF THE INVENTION

The present invention relates to the exhaust gas emitted from aturbomachine, and more particularly to a system for reducing the harmfulconstituents within the exhaust gas before recirculating the exhaust gasback into the turbomachine.

There is a growing concern over the long-term effects of Nitrous Oxide(hereinafter NOx) and Carbon Dioxide (hereinafter “CO₂”) and Sulfuremissions on the environment. The allowable levels of NOx and CO₂ thatmay be emitted by a turbomachine, such as a gas turbine are heavilyregulated. Operators of turbomachines desire methods of reducing thelevels of NOx and CO₂ emitted.

Exhaust gas recirculation (EGR) generally involves recirculating aportion of the emitted exhaust through an inlet portion of theturbomachine where it is mixing with the incoming airflow prior tocombustion. This process facilitates the removal and sequestration ofthe emitted NOx and concentrated CO₂ levels, thereby reducing the netemission levels.

There are a few problems with the currently known EGR systems.Impurities and moisture within the exhaust gas prevent utilizing asimple re-circulating loop to reduce the CO₂ and NOx reduction. Turbinefouling, corrosion, and accelerated wear of internal turbomachinecomponents would result from introducing the exhaust gas directly to theturbomachine inlet portion. As a result, the diverted exhaust gas shouldbe treated prior to blending with the inlet air. Significant amounts ofcondensable vapors exist in the exhaust gas stream. These vapors usuallycontain a variety of constituents such as water vapor, acids, aldehydes,hydrocarbons, sulfur, and chlorine compounds. Left untreated, theseconstituents will accelerate corrosion and the fouling of the internalcomponents if allowed to enter the inlet of a gas turbine.

For the foregoing reasons, there is a need for system for treating there-circulated exhaust gas stream to minimize the impact of harmfulconstituents within the exhaust gas stream on turbomachine components.

BRIEF DESCRIPTION OF THE INVENTION

In accordance with an embodiment of the present invention, a system forreducing constituents within at least one exhaust stream of at least oneturbomachine comprising an inlet portion and an exhaust portion; thesystem comprising: providing at least one exhaust gas recirculationsystem (EGR) comprising at least one scrubber; wherein the at least onescrubber can: receive the at least one exhaust stream at a firsttemperature from the exhaust portion of the at least one turbomachine;receive the at least one exhaust stream comprising constituents at afirst level; reduce the constituents to a second level; and allow the atleast one exhaust stream to exit at a second temperature; and whereinthe at least one exhaust stream is a portion of the total exhaustexiting the at least one turbomachine; and wherein the at least one EGRrecirculates the at least one exhaust stream exiting the at least onescrubber to the inlet portion.

BRIEF DESCRIPTION OF THE DRAWINGS

FIG. 1 is a schematic illustrating an example of a system forrecirculating the exhaust of a turbomachine in accordance with anembodiment of the present invention.

FIG. 2 is a schematic illustrating an example of a system forrecirculating the exhaust of a turbomachine in accordance with a secondembodiment of the present invention.

FIG. 3 is a schematic illustrating an example of a system forrecirculating the exhaust of a turbomachine in accordance with a thirdembodiment of the present invention.

FIG. 4 is a schematic illustrating an example of a system forrecirculating the exhaust of a turbomachine in accordance with a fourthembodiment of the present invention.

FIG. 5 is a schematic illustrating an example of a system forrecirculating the exhaust of a turbomachine in accordance with a fifthembodiment of the present invention.

DETAILED DESCRIPTION OF THE INVENTION

The following detailed description of preferred embodiments refers tothe accompanying drawings, which illustrate specific embodiments of theinvention. Other embodiments having different structures and operationsdo not depart from the scope of the present invention.

Certain terminology is used herein for the convenience of the readeronly and is not to be taken as a limitation on the scope of theinvention. For example, words such as “upper,” “lower,” “left,” “right,”“front”, “rear” “top”, “bottom”, “horizontal,” “vertical,” “upstream,”“downstream,” “fore”, “aft”, and the like; merely describe theconfiguration shown in the Figures. Indeed, the element or elements ofan embodiment of the present invention may be oriented in any directionand the terminology, therefore, should be understood as encompassingsuch variations unless specified otherwise.

An embodiment of the present invention takes the form of a system thatmay recirculate a portion of the exhaust of at least one turbomachinewhere it may be mixed with the inlet air and re-enter the turbomachinewithout affecting reliability and availability of the unit.

Generally, the exhaust gas recirculation system of an embodiment of thepresent invention comprises of multiple elements. The configuration andsequence of the elements may be dictated by the composition of theexhaust gas. In general the steps comprising the exhaust gasre-circulation process are; cooling, scrubbing, de-misting, highefficiency particulate and droplet removal, and mixing. When the presentinvention is utilized, the diverted gas, blended with inlet air, can beintroduced to the turbine inlet without harm. As described below, thereare multiple arrangements that may be used to accomplish the exhaust gastreatment.

The present invention has the technical effect of reducing the levels ofNOx, concentrated CO₂, and harmful constituents, all of which may bewithin a portion of the exhaust (hereinafter “exhaust stream”, or thelike). These levels may be reduced from a first level to a second levelthat may be determined by an operator of the turbomachine. An embodimentof the present invention may also allow for the removal andsequestration of concentrated CO₂ emissions.

The present invention may be applied to the variety of turbomachinesthat produce a gaseous fluid, such as, but not limiting of, a heavy dutygas turbine: an aero-derivative gas turbine; or the like (hereinafterreferred to as “gas turbine”). An embodiment of the present inventionmay be applied to either a single gas turbine or a plurality of gasturbines. An embodiment of the present invention may be applied to a gasturbine operating in a simple cycle or a combined cycle configuration.

As described below, an embodiment of the present invention may utilizeat least one scrubber; or at least one scrubber and at least onedownstream heat exchanger; or at least one scrubber and at least oneupstream heat exchanger; or at least one scrubber, at least onedownstream heat exchanger; and at least one upstream heat exchanger; orvarious combinations thereof. Moreover, each and any of theaforementioned embodiments may include an injector that may introduce areagent for reducing the level of harmful constituents within theexhaust stream; and a wet electrostatic precipitator for removing theconstituents.

The elements of the present invention, such as, but not limiting of, ascrubber and a heat exchanger may be fabricated of any materials thatcan withstand the operating environment under which the exhaust gasrecirculation system may function and operate.

Referring now to the Figures, where the various numbers represent likeelements throughout the several views, FIG. 1 is a schematicillustrating an example of a system for recirculating the exhaust of aturbomachine in accordance with an embodiment of the present invention.FIG. 1 illustrates a gas turbine 100 and an exhaust gas recirculationsystem 150.

The gas turbine 100 comprises a compressor 110 having a shaft 120. Airenters the inlet of the compressor at 125, is compressed by thecompressor 110 and is then discharged to a combustion system 130, wherea fuel 135 such as, but not limiting of, natural gas is burned toprovide high-energy combustion gases which drive the turbine 145. In theturbine 145, the energy of the hot gases is converted into work, some ofwhich is used to drive the compressor 110 through the shaft 120, withthe remainder being available for useful work to drive a load (notillustrated).

The exhaust gas recirculation system 150, as illustrated in FIG. 1,comprises at least one EGR flow modulation device 155 and at least onescrubber 170.

The at least one EGR flow modulation device 155 may apportion the totalexhaust flow (not illustrated in FIG. 1) between a non-recirculatedexhaust 160 and at least one exhaust stream 165. The at least one EGRflow modulation device 155 may be of a size and fabricated of a materialcapable of withstanding the physical properties, such as, but notlimiting of, a flowrate of about 10000 Lb/hr to about 50000000 Lb/hr anda temperature of about 100 F to about 1500 F.

An operator of the gas turbine 100, may determine the position of the atleast one EGR flow modulation device 155 based on the desired flowrateof the at least one exhaust stream 165. The at least one exhaust stream165 may flow downstream of the at least one EGR flow modulation device155 to an inlet portion of the at least one scrubber 170.

A scrubber system (hereinafter “scrubber”) is generally considered as anair pollution control device that may remove particulates and/or otheremissions from industrial exhaust streams. A scrubber may use a“scrubbing process”, or the like, involving a liquid to “scrub” unwantedpollutants from a gas stream.

In an embodiment of the present invention the at least one scrubber 170may perform a few functions after receiving the at least one exhauststream 165. The at least one scrubber 170 may lower the temperature ofthe at least one exhaust stream 165 to a range of about 60 degreesFahrenheit to about 100 degrees Fahrenheit. The at least one scrubber170 may also remove a portion of the plurality of constituents (notillustrated) within the at least one exhaust stream 165, from a firstlevel to a second level. In an embodiment of the present invention anoperator of the at least one turbomachine may determine requirements ofthe second level. The constituents may include for example, but notlimiting of, at least one of: water vapor, acids, aldehydes,hydrocarbons, or combinations thereof.

The at least one scrubber 170 may receive and then later discharge ascrubber cooling fluid 172,174; which may be of a type that allows forthe heat transfer required to lower the temperature of the at least oneexhaust stream 165, as discussed.

The at least one scrubber 170 may include at least one scrubber blowdown line 176; which may remove the portion of the aforementionedconstituents and concentrated CO₂. The condensable line 178 may removethe portions of at least one exhaust stream 165 that may condense duringthe scrubbing process. The scrubber recirculation line 180 mayrecirculate a portion of the at least one exhaust stream 165 to increasethe effectiveness of the scrubbing process.

After the scrubbing process, the at least one exhaust stream 165 mayflow downstream to the compressor 110. The exhaust gas recirculationsystem 150 may then mix the inlet air 125 with the at least one exhauststream 165, prior to the compression performed by the compressor 110.

In use, the exhaust gas recirculation system 150 of the above describedembodiment of the present invention functions while the gas turbine 100is in operation. The EGR flow modulation device 155 may be positioned toallow for the desired flowrate of the at least one exhaust stream 165,and the non-recirculated exhaust 160 may flow through an exhaust stack(not illustrated), or the like or elsewhere such as, but not limitingof, a heat recovery steam generator (not illustrated). The at least oneexhaust stream 165 may then flow downstream through the at least onescrubber 170, as described above. In the at least one scrubber 170, thetemperature of the at least one exhaust stream 165, may be lowered tobelow the saturation temperature. The use of the scrubber cooling fluid172,174 and the drop in temperature of the at least one exhaust stream165, may cause a portion of the at least one exhaust stream 165 to flowthrough the scrubber recirculation line 180. Here, a portion ofcondensable vapors of the at least one exhaust stream 165 may be removedvia the condensable line 178. Next, the at least one exhaust stream 165may flow downstream of the at least one scrubber 170 and into thecompressor 110.

The alternate embodiments of the present invention discussed below, andillustrated in FIGS. 2 through 5, modify the flow path of the at leastone exhaust stream 165 and the configuration of the exhaust gasrecirculation system 150. The discussion of each embodiment willemphasize the differences from the embodiment discussed above.Furthermore, FIGS. 2 through 5 illustrate the at least one gas turbine100 configured for a combined cycle operation. Here, a heat recoverysteam generator (HRSG) 200 receives the total exhaust of the gas turbine100. As illustrated in FIGS. 2 through 5, the EGR flow modulation device155 may be connected downstream of the HRSG 200 and function aspreviously described.

FIG. 2 is a schematic illustrating an example of a system forrecirculating the exhaust of a turbomachine in accordance with a secondembodiment of the present invention. In this second embodiment of thepresent invention, the exhaust gas recirculation system 150 may include:at least one scrubber 170, at least one downstream heat exchanger 220;at least one de-mister 230; and at least one mixing station 240.

The at least one scrubber 170, in this second embodiment of the presentscrubber 170, may reduce the temperature of the at least one exhauststream 165 and may also remove a portion of the plurality ofconstituents (not illustrated) within the at least one exhaust stream165, as described.

The at least one scrubber 170 may include at least one scrubber blowdown line 176; and at least one scrubber recirculation line 180, asdescribed. The at least one scrubber 170 may also include at least onescrubber make-up line 210 which may supply a fluid used in the scrubbingprocess.

The at least one downstream heat exchanger 220 may be located downstreamof the at least one scrubber 170 may cool the at least one exhauststream 165 down to a reasonable temperature such that the performance ofthe gas turbine 100 may not be impacted due to a hot inlet air 130temperature. For example, but not limiting of, the at least onedownstream heat exchanger 220 may reduce the temperature of the at leastone exhaust stream 165 to a range of about 35 degrees (roughly above afreezing temperature) Fahrenheit to about 100 degrees Fahrenheit.

The at least one downstream heat exchanger 220 may receive and thenlater discharge a downstream cooling fluid 222,224; which may be of atype that allows for the amount of heat transfer required to lower thetemperature of the at least one exhaust stream 165, as discussed.

The at least one downstream heat exchanger 220 may also include at leastone condensable line 178, which may remove the portions of at least oneexhaust stream 165 that may condense during the heat exchanging process.

The at least one de-mister 230 may be located downstream of the at leastone downstream heat exchanger 220 in this second embodiment of thepresent invention. The at least one de-mister 230 may remove droplets ofwater from the at least one exhaust stream 165 that may have carriedfrom the scrubbing and the heat exchanging processes.

As discussed, an embodiment of the present invention may include the atleast one mixing station 240, which may be located downstream of the atleast one downstream heat exchanger 220. The at least one mixing station240, may be considered a device which mixes the inlet air 125 and the atleast one exhaust stream 165, and forms an inlet fluid 250 that entersthe compressor 240.

The at least one mixing station 240 may utilize, for example, but notlimiting of, baffles, flow turners, or the like, to mix the inlet air125 with the at least one exhaust stream 165.

As illustrated in FIG. 1, an embodiment of the present invention may notrequire the at least one mixing station 240. Here, for example, but notlimiting of, the inlet air 125 and the at least one exhaust stream 165,may mix within an area adjacent the compressor 110, such as, but notlimiting of, an inlet duct, in the plenum, near the inlet filter house,or the like.

In use, the exhaust gas recirculation system 150 of the secondembodiment of the present invention functions while the gas turbine 100is in operation. The EGR flow modulation device 155 may be positioned toallow for the desired flowrate of the at least one exhaust stream 165,as previously described. The at least one exhaust stream 165 may thenflow downstream through the at least one scrubber 170, as describedabove. In the at least one scrubber 170, the temperature of the at leastone exhaust stream 165 may be lower to below the saturation temperature.The use of the scrubber cooling fluid 172,174, and the drop intemperature of the at least one exhaust stream 165, may cause a portionof the stream 165 to flow through the scrubber recirculation line 180. Aportion of the fluid used within the scrubber 170 may be replaced withfresh fluid via the scrubber make-up line 210.

Next, the at least one exhaust stream 165 may flow downstream of the atleast one scrubber 170 to the at least one downstream heat exchanger220, where a portion of condensable vapors of the at least one exhauststream 165 from be removed via the condensable line 178. Next, the atleast one exhaust stream 165 may flow through the at least one de-mister230, and then into the at least one mixing station 240, all of which aredescribed above. Downstream of the at least one mixing station 240, theinlet fluid 250 may flow into the compressor 110. This second embodimentof the present invention allows for an alternate configuration of the atleast one de-mister 230 and the at least one mixing station 240. Forexample, but not limiting of, the exhaust gas recirculation system 150may be configured such that the at least one mixing station 240 islocated immediately downstream of the at least one downstream heatexchanger 220; and therefore the at least one de-mister 230 is locateddownstream of the at least one mixing station 240.

FIG. 3 is a schematic illustrating an example of a system forrecirculating the exhaust of a turbomachine in accordance with a thirdembodiment of the present invention. The key difference between thisthird embodiment and the second embodiment of the present invention iswhere the at least one heat exchanger is located within the exhaust gasrecirculation system 150. As previously discussed, the second embodimentof the present invention may include at least one downstream heatexchanger 220 located downstream of the at least one scrubber 170.However, the third embodiment of the present invention, discussed below,may include at least one upstream heat exchanger 300 located upstream ofthe at least one scrubber 170. In this third embodiment of the presentinvention, the exhaust gas recirculation system 150 may include: atleast one scrubber 170, at least one upstream heat exchanger 300; atleast one de-mister 230; and at least one mixing station 240.

The at least one upstream heat exchanger 300 may be located upstream ofthe at least one scrubber 170, and may receive the at least one exhauststream 165 exiting the EGR flow modulation device 155. The at least oneupstream heat exchanger 300 may cool the at least one exhaust stream 165to a range of about 60 degrees Fahrenheit to about 100 degreesFahrenheit.

The at least one upstream heat exchanger 300 may receive and then laterdischarge a upstream cooling fluid 302,304; which may be of a type thatallows for the amount of heat transfer required to lower the temperatureof the at least one exhaust stream 165, as discussed.

The at least one upstream heat exchanger 300 may also include at leastone condensable line 178, which may remove portions of the at least oneexhaust stream 165 that may condense during the heat exchanging process.

In use, the exhaust gas recirculation system 150 of the third embodimentof the present invention functions while the gas turbine 100 is inoperation. The EGR flow modulation device 155 may be positioned to allowfor the desired flowrate of the at least one exhaust stream 165, aspreviously described. The at least one exhaust stream 165 may then flowdownstream through the at least one upstream heat exchanger 300, where apotion of condensable vapors of the at least one exhaust stream 165 maybe removed via the condensable line 178.

Next, the at least one exhaust stream 165 may flow downstream throughthe at least one scrubber 170, as described above. Next, the at leastone exhaust stream 165 may flow downstream of the at least one scrubber170 to the at least one de-mister 230, and then into the at least onemixing station 240, all of which are described above. Downstream of theat least one mixing station 240, the inlet fluid 250 may flow into thecompressor 110. The third embodiment of the present invention allows foran alternate configuration of at least one de-mister 230 and the atleast one mixing station 240. For example, but not limiting of, theexhaust gas recirculation system 150 may be configured such that the atleast one mixing station 240 is located immediately downstream of the atleast one downstream heat exchanger 220; and therefore the at least onede-mister 230 is located downstream of the at least one mixing station240.

FIG. 4 is a schematic illustrating an example of a system forrecirculating the exhaust of a turbomachine in accordance with a fourthembodiment of the present invention. The configuration of this fourthembodiment of the present invention may allow the heat removal in the atleast one exhaust stream 165 to be accomplished be multiple heatexchangers located up and down stream of the at least one scrubber 170.This configuration may allow for relatively smaller heat exchangers thanthose of the previously described embodiments.

The key difference between this fourth embodiment and the second andthird embodiments of the present invention is the inclusion of both theat least one downstream heat exchanger 220 and at least one upstreamheat exchanger 300 within the exhaust gas recirculation system 150. Inthis fourth embodiment of the present invention, the exhaust gasrecirculation system 150 may include: at least one scrubber 170, atleast one upstream heat exchanger 300; at least one downstream heatexchanger 220; at least one de-mister 230; and at least one mixingstation 240.

The fourth embodiment of the present invention may integrate theoperation of the at least one upstream heat exchanger 300, at least onedownstream heat exchanger 220, and at least one scrubber 170; to removeheat from, and thus lower the temperature of, the at least one exhauststream 165 in stages, as described next.

In use, the exhaust gas recirculation system 150 of the fourthembodiment of the present invention functions while the gas turbine 100is in operation. The EGR flow modulation device 155 may be positioned toallow for the desired flowrate of the at least one exhaust stream 165,as previously described. The at least one exhaust stream 165 may thenflow downstream through the at least one upstream heat exchanger 300,which may lower the temperature of the at least one exhaust stream 165to a range of about 120 degrees Fahrenheit to about 150 degreesFahrenheit. Next, the at least one exhaust stream 165 may then flowdownstream to the at least one scrubber 170, as described above. Next,the at least one exhaust stream 165 may flow downstream of the at leastone scrubber 170 through the at least one downstream heat exchanger 220,which may lower the temperature of the at least one exhaust stream 165to a range of about 60 degrees Fahrenheit to about 100 degreesFahrenheit. Next, the at least one exhaust stream 165 may flow throughthe at least one de-mister 230, and then into the at least one mixingstation 240, all of which are described above. Downstream of the atleast one mixing station 240, the inlet fluid 250 may flow into thecompressor 110. The fourth embodiment of the present invention allowsfor an alternate configuration of at least one de-mister 230 and the atleast one mixing station 240, as described above.

The fourth embodiment of the present invention may also allow for analternate staging of the heat removal from the at least one exhauststream 165. For example, but not limiting of, the at least one upstreamheat exchanger 300 may lower the temperature of the at least one exhauststream 165 to a range of about 150 degrees Fahrenheit to about 350degrees Fahrenheit; next the at least one scrubber 170 may lower thetemperature to about 120 degrees Fahrenheit to about 150 degreesFahrenheit; and then the at least one downstream heat exchanger 220 maylower the temperature to about 60 degrees Fahrenheit to about 100degrees Fahrenheit.

FIG. 5 is a schematic illustrating an example of a system forrecirculating the exhaust of a turbomachine in accordance with a fifthembodiment of the present invention. The key difference between thisfifth embodiment and the fourth embodiment of the present invention isthe inclusion of at least one injector 500 and at least one wetelectrostatic precipitator 510. As discussed, the at least one scrubber170 may use a fluid in scrubbing process to remove a portion of theconstituents within at least one exhaust stream 165. Due to the make-upof the constituents a reagent may be required to assist in the removalof the constituents. The reagent may perform an absorption process toremove the constituents. The reagent may include for example, but notlimiting of, an ammonia, a limestone based liquid reagent, water, or thelike, and combinations thereof. The at least one injector 500 may injectthe reagent into the at least one scrubber 170 of the exhaust gasrecirculation system 150.

The absorption process used by the reagent may create a particulatematter that should be removed from the at least one scrubber 170. The atleast one wet electrostatic precipitator 510 may remove the particulatematter. Generally the wet electrostatic precipitator 510 may induce anelectrostatic charge and utilize a fluid to perform a scrubbing likeaction, in removing particulate matter from the at least one scrubber170.

The at least one injector 500 and at least one wet electrostaticprecipitator 510 may be added to any of the previous embodiments. Asdiscussed below, the at least one injector 500 and at least one wetelectrostatic precipitator 510 may be utilized when the condensing andscrubbing processes previously described do not reduce the constituentswithin the at least one exhaust stream 165 to the second level.

In the fifth embodiment of the present invention, as illustrated in FIG.5, the exhaust gas recirculation system 150 may include: at least onescrubber 170; at least one injector 500; at least one upstream heatexchanger 300; at least one downstream heat exchanger 220; at least onewet electrostatic precipitator 510; at least one de-mister 230; and atleast one mixing station 240.

In use, the exhaust gas recirculation system 150 of the fifth embodimentof the present invention, as illustrated in FIG. 5, functions while thegas turbine 100 is in operation. The EGR flow modulation device 155 maybe positioned to allow for the desired flowrate of the at least oneexhaust stream 165, as previously described. The at least one exhauststream 165 may flow downstream through at least one upstream heatexchanger 300, which may lower the temperature of the at least oneexhaust stream 165 to a range of about 120 degrees Fahrenheit to about150 degrees Fahrenheit. Next, the at least one exhaust stream 165 maythen flow downstream to the at least one scrubber 170, to the at leastone injector 500 may inject at least one reagent, as described. Next,the at least one exhaust stream 165 may flow downstream of the at leastone scrubber 170 through the at least one downstream heat exchanger 220,which may lower the temperature of the at least one exhaust stream 165to a range of about 60 degrees Fahrenheit to about 100 degreesFahrenheit.

Next, the at least one exhaust stream 165 may flow through the at leastone wet electrostatic precipitator 510, then the at least one de-mister230, and then into the at least one mixing station 240, all of which aredescribed above. Downstream of the at least one mixing station 240, theinlet fluid 250 may flow into the compressor 110.

The fifth embodiment of the present invention allows for an alternateconfiguration of at least one de-mister 230 and the at least one mixingstation 240, as described above. The fifth embodiment of the presentinvention may also allow for an alternate staging of the heat removalfrom the at least one exhaust stream 165, as described.

The terminology used herein is for the purpose of describing particularembodiments only and is not intended to be limiting of the invention. Asused herein, the singular forms “a”, “an” and “the” are intended toinclude the plural forms as well, unless the context clearly indicatesotherwise. It will be further understood that the terms “comprises”and/or “comprising,” when used in this specification, specify thepresence of stated features, integers, steps, operations, elements,and/or components, but do not preclude the presence or addition of oneor more other features, integers, steps, operations, elements,components, and/or groups thereof.

Although specific embodiments have been illustrated and describedherein, it should be appreciated that any arrangement, which iscalculated to achieve the same purpose, may be substituted for thespecific embodiments shown and that the invention has other applicationsin other environments. This application is intended to cover anyadaptations or variations of the present invention. The following claimsare in no way intended to limit the scope of the invention to thespecific embodiments described herein.

1. A system for reducing constituents within at least one exhaust stream of at least one turbomachine comprising an inlet portion and an exhaust portion; the system comprising: providing at least one exhaust gas recirculation system (EGR) comprising at least one scrubber; wherein the at least one scrubber can: receive the at least one exhaust stream at a first temperature from the exhaust portion of the at least one turbomachine; receive the at least one exhaust stream comprising constituents at a first level; reduce the constituents to a second level; and allow the at least one exhaust stream to exit at a second temperature; and wherein the at least one exhaust stream is a portion of the total exhaust exiting the at least one turbomachine; and wherein the at least one EGR recirculates the at least one exhaust stream exiting the at least one scrubber to the inlet portion.
 2. The system of claim 1, further comprising at least one heat recovery steam generator (HRSG) installed downstream of the exhaust portion and upstream of the at least one scrubber; wherein the at least one exhaust stream flows from the exhaust portion of the at least one turbomachine to an inlet portion of the HRSG and then flows from an outlet portion of the HRSG to an inlet portion of the at least one scrubber.
 3. The system of claim 1, wherein the constituents comprise at least one of: water, acids, aldehydes, hydrocarbons, or combinations thereof.
 4. The system of claim 1, wherein the at least one exhaust stream exiting comprises a flowrate of about 10,000 Lb/hr to about 50,000,000 pounds per hour and a temperature of about 100 degrees Fahrenheit to about 1500 degrees Fahrenheit.
 5. The system of claim 1, further comprising at least one EGR flow modulation device for diverting the at least one exhaust stream from the total exhaust existing the at least one turbomachine.
 6. The system of claim 5, further comprising: at least one downstream heat exchanger; wherein the at least one downstream heat exchanger receives the at least one exhaust stream from an outlet portion of the at least one scrubber and reduces the temperature of the at least one exhaust stream; at least one de-mister; wherein the at least one de-mister is connected downstream of the at least one downstream heat exchanger and removes water from the at least one exhaust stream; and at least one mixing station; wherein the at least one mixing station is connected upstream of the inlet portion of the at least one turbomachine and mixes the at least one exhaust stream with an inlet air, wherein the inlet air is entering the at least one turbomachine.
 7. The system of claim 6, wherein the temperature of the at least one exhaust stream existing the at least one downstream heat exchanger is about 60 degrees Fahrenheit to about 100 degrees Fahrenheit; and wherein the temperature of the of the at least one exhaust stream entering the inlet portion is about 60 degrees Fahrenheit to about 100 degrees Fahrenheit.
 8. The system of claim 7, further comprising: at least one injector for injecting at least one reagent into the at least one scrubber for absorbing a portion of the constituents in the at least one exhaust stream; and at least one wet electrostatic precipitator, wherein the at least one wet electrostatic precipitator is connected downstream of the at least one downstream heat exchanger and removes a portion of the constituents in the at least one exhaust stream.
 9. The system of claim 5, further comprising: at least one upstream heat exchanger; wherein the at least one upstream heat exchanger can: receive the at least one exhaust stream; reduce the temperature of the at least one exhaust stream; and allow the at least one exhaust stream to flow to an inlet portion of the at least one scrubber; at least one de-mister; wherein the at least one de-mister is connected downstream of the at least one scrubber and removes water from the at least one exhaust stream; and at least one mixing station; wherein the at least one mixing station is connected upstream of the inlet portion of the at least one turbomachine and mixes the at least one exhaust stream with an inlet air entering the at least one turbomachine.
 10. The system of claim 9, wherein the temperature of the at least one exhaust stream existing the at least one upstream heat exchanger is about 60 degrees Fahrenheit to about 100 degrees Fahrenheit.
 11. The system of claim 9, further comprising: at least one injector for injecting at least one reagent into the at least one scrubber for absorbing a portion of the constituents in the at least one exhaust stream; and at least one wet electrostatic precipitator, wherein the at least one wet electrostatic precipitator is connected downstream of the at least one downstream heat exchanger and removes a portion of the constituents in the at least one exhaust stream.
 12. The system of claim 5, further comprising: at least one upstream heat exchanger; wherein the at least one upstream heat exchanger can: receive the at least one exhaust stream; reduce the temperature of the at least one exhaust stream; and allow the at least one exhaust stream to flow to an inlet portion of the at least one scrubber; at least one downstream heat exchanger; wherein the at least one downstream heat exchanger receives the at least one exhaust stream from an outlet portion of the at least one scrubber and reduces the temperature of the at least one exhaust stream; at least one de-mister; wherein the at least one de-mister is connected downstream of the at least one downstream heat exchanger and removes water from the at least one exhaust stream; and at least one mixing station; wherein the at least one mixing station is connected upstream of the inlet portion of the at least one turbomachine and mixes the at least one exhaust stream with an inlet air entering the at least one turbomachine.
 13. The system of claim 12, wherein the temperature of the at least one exhaust stream existing the at least one upstream heat exchanger is about 120 degrees Fahrenheit to about 150 degrees Fahrenheit; and wherein the of the temperature at least one exhaust stream existing the at least one downstream heat exchanger is about 60 degrees Fahrenheit to about 100 degrees Fahrenheit.
 14. The system of claim 12, wherein the temperature of the at least one exhaust stream existing the at least one upstream heat exchanger is about 150 degrees Fahrenheit to about 1000 degrees Fahrenheit; wherein the temperature of the at least one exhaust stream exiting the at least one scrubber is about 120 degrees Fahrenheit to about 150 degrees Fahrenheit; and wherein the of the at least one exhaust stream existing the at least one downstream heat exchanger is about 60 degrees Fahrenheit to about 100 degrees Fahrenheit.
 15. The system of claim 14, further comprising: at least one injector for injecting at least one reagent into the at least one scrubber for absorbing a portion of the constituents in the at least one exhaust stream.
 16. The system of claim 5, further comprising: at least one injector for injecting at least one reagent into the at least one scrubber for absorbing a portion of the constituents in the at least one exhaust stream; at least one upstream heat exchanger; wherein the at least one upstream heat exchanger can: receive the at least one exhaust stream; reduce the temperature of the at least one exhaust stream; and allow the at least one exhaust stream to flow to an inlet portion of the at least one scrubber; at least one downstream heat exchanger; wherein the at least one downstream heat exchanger receives the at least one exhaust stream from an outlet portion of the at least one scrubber and reduces the temperature of the at least one exhaust stream; at least one wet electrostatic precipitator, wherein the at least one wet electrostatic precipitator is connected downstream of the at least one downstream heat exchanger and removes a portion of the constituents in the at least one exhaust stream; at least one de-mister; wherein the at least one de-mister is connected downstream of the at least one downstream heat exchanger and removes water from the at least one exhaust stream; and at least one mixing station; wherein the at least one mixing station is connected upstream of the inlet portion of the at least one turbomachine and mixes the at least one exhaust stream with an inlet air entering the at least one turbomachine.
 17. The system of claim 16, wherein the temperature of the at least one exhaust stream existing the at least one upstream heat exchanger is about 120 degrees Fahrenheit to about 150 degrees Fahrenheit; and wherein the of the temperature at least one exhaust stream existing the at least one downstream heat exchanger is about 60 degrees Fahrenheit to about 100 degrees Fahrenheit.
 18. The system of claim 17, wherein the temperature of the at least one exhaust stream existing the at least one upstream heat exchanger is about 150 degrees Fahrenheit to about 1000 degrees Fahrenheit; wherein the temperature of the at least one exhaust stream exiting the at least one scrubber is about 120 degrees Fahrenheit to about 150 degrees Fahrenheit; and wherein the of the at least one exhaust stream existing the at least one downstream heat exchanger is about 60 degrees Fahrenheit to about 100 degrees Fahrenheit. 